EP2774674A1 - Wasserunlösliche Rutheniumkatalysatorzusammensetzung zur Verwendung bei wässrigen Hydrierungsreaktionen - Google Patents

Wasserunlösliche Rutheniumkatalysatorzusammensetzung zur Verwendung bei wässrigen Hydrierungsreaktionen Download PDF

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EP2774674A1
EP2774674A1 EP13157998.9A EP13157998A EP2774674A1 EP 2774674 A1 EP2774674 A1 EP 2774674A1 EP 13157998 A EP13157998 A EP 13157998A EP 2774674 A1 EP2774674 A1 EP 2774674A1
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water
surfactant
solvent system
phosphane
diphenyl
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French (fr)
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Sonja Jost
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Priority to EP13157998.9A priority Critical patent/EP2774674A1/de
Priority to JP2015560679A priority patent/JP6423805B2/ja
Priority to US14/772,393 priority patent/US9433937B2/en
Priority to EP14713774.9A priority patent/EP2964384B1/de
Priority to PCT/EP2014/054291 priority patent/WO2014135605A1/en
Priority to HUE14713774A priority patent/HUE059503T2/hu
Priority to CN201480024756.8A priority patent/CN105392563B/zh
Priority to DK14713774.9T priority patent/DK2964384T3/da
Priority to ES14713774T priority patent/ES2922331T3/es
Priority to PL14713774.9T priority patent/PL2964384T3/pl
Publication of EP2774674A1 publication Critical patent/EP2774674A1/de
Priority to IL241130A priority patent/IL241130B/en
Priority to US15/243,980 priority patent/US9758457B2/en
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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
    • C07C29/136—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH
    • C07C29/143—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of ketones
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/24—Phosphines, i.e. phosphorus bonded to only carbon atoms, or to both carbon and hydrogen atoms, including e.g. sp2-hybridised phosphorus compounds such as phosphabenzene, phosphole or anionic phospholide ligands
    • B01J31/2404—Cyclic ligands, including e.g. non-condensed polycyclic ligands, the phosphine-P atom being a ring member or a substituent on the ring
    • B01J31/2409—Cyclic ligands, including e.g. non-condensed polycyclic ligands, the phosphine-P atom being a ring member or a substituent on the ring with more than one complexing phosphine-P atom
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/24—Phosphines, i.e. phosphorus bonded to only carbon atoms, or to both carbon and hydrogen atoms, including e.g. sp2-hybridised phosphorus compounds such as phosphabenzene, phosphole or anionic phospholide ligands
    • B01J31/2404—Cyclic ligands, including e.g. non-condensed polycyclic ligands, the phosphine-P atom being a ring member or a substituent on the ring
    • B01J31/2442—Cyclic ligands, including e.g. non-condensed polycyclic ligands, the phosphine-P atom being a ring member or a substituent on the ring comprising condensed ring systems
    • B01J31/2447—Cyclic ligands, including e.g. non-condensed polycyclic ligands, the phosphine-P atom being a ring member or a substituent on the ring comprising condensed ring systems and phosphine-P atoms as substituents on a ring of the condensed system or on a further attached ring
    • B01J31/2452—Cyclic ligands, including e.g. non-condensed polycyclic ligands, the phosphine-P atom being a ring member or a substituent on the ring comprising condensed ring systems and phosphine-P atoms as substituents on a ring of the condensed system or on a further attached ring with more than one complexing phosphine-P atom
    • B01J31/2457—Cyclic ligands, including e.g. non-condensed polycyclic ligands, the phosphine-P atom being a ring member or a substituent on the ring comprising condensed ring systems and phosphine-P atoms as substituents on a ring of the condensed system or on a further attached ring with more than one complexing phosphine-P atom comprising aliphatic or saturated rings, e.g. Xantphos
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
    • C07C29/136—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH
    • C07C29/143—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of ketones
    • C07C29/145—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of ketones with hydrogen or hydrogen-containing gases
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00—Preparation of carboxylic acid esters
    • C07C67/30—Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group
    • C07C67/31—Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group by introduction of functional groups containing oxygen only in singly bound form
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F15/00—Compounds containing elements of Groups 8, 9, 10 or 18 of the Periodic Table
    • C07F15/0006—Compounds containing elements of Groups 8, 9, 10 or 18 of the Periodic Table compounds of the platinum group
    • C07F15/0046—Ruthenium compounds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
    • B01J2231/60—Reduction reactions, e.g. hydrogenation
    • B01J2231/64—Reductions in general of organic substrates, e.g. hydride reductions or hydrogenations
    • B01J2231/641—Hydrogenation of organic substrates, i.e. H2 or H-transfer hydrogenations, e.g. Fischer-Tropsch processes
    • B01J2231/643—Hydrogenation of organic substrates, i.e. H2 or H-transfer hydrogenations, e.g. Fischer-Tropsch processes of R2C=O or R2C=NR (R= C, H)
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/02—Compositional aspects of complexes used, e.g. polynuclearity
    • B01J2531/0261—Complexes comprising ligands with non-tetrahedral chirality
    • B01J2531/0266—Axially chiral or atropisomeric ligands, e.g. bulky biaryls such as donor-substituted binaphthalenes, e.g. "BINAP" or "BINOL"
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/80—Complexes comprising metals of Group VIII as the central metal
    • B01J2531/82—Metals of the platinum group
    • B01J2531/821—Ruthenium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/90—Catalytic systems characterized by the solvent or solvent system used
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/90—Catalytic systems characterized by the solvent or solvent system used
    • B01J2531/96—Water
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
    • C07B2200/00—Indexing scheme relating to specific properties of organic compounds
    • C07B2200/07—Optical isomers

Definitions

  • the present invention relates to a method for converting an inactive ruthenium precatalyst into an active catalyst in aqueous solutions.
  • the present invention further relates to a method for manufacturing a water-insoluble chiral catalyst, and to its use.
  • Pure enantiomers are used in the synthesis of, inter alia, pharmaceuticals, agrochemicals, flavours and fragrances.
  • Asymmetric chemocatalysis is an efficient production method for chiral molecules.
  • Current large-scale protocols however, rely on the use of organic solvents, making these methods expensive and problematic from a safety and environmental impact point of view.
  • Rhodium-catalyzed asymmetric hydrogenations of different substrates in aqueous/surfactant media and/or biphasic systems have been explored by Grassert et al. (J. Organomet. Chem., 621, pages 158-165, 2001 ) they show a 1,5-cyclooctadiene)bismethylallylrhodium phosphine complex.
  • the ligands used in aqueous solutions differ from conventional chiral ligands -which are insoluble in water- by the addition of chemical groups to render them water soluble. This modification is expensive.
  • water-insoluble catalysts can be made and used in aqueous media, particularly in the absence of any organic solvent. It was further found that such catalyst can be activated in aqueous media.
  • the present invention provides a method for converting a precatalyst complex to an active catalyst complex, wherein the precatalyst complex comprises a ruthenium atom and an optically active ligand, and wherein the active catalyst complex comprises the ruthenium atom, the optically active ligand, a monohydride and at least one water molecule, and wherein the monohydride and the water molecule are bound to said ruthenium atom, and wherein the optically active ligand is insoluble in water.
  • the nature of the bond between the ruthenium atom and the water molecule or the monohydride is covalent or coordinative in nature.
  • the method of the invention comprises the steps of providing water as an activation solvent system, and solving the precatalyst complex an acid, and hydrogen in the activation solvent system at a pH value of the activation solvent system equal or below 2.
  • a method for converting a precatalyst complex to an active catalyst complex is provided,
  • a precatalyst complex in the context of the present specification refers particularly to a complex comprising an optically active ligand that (the ligand) is insoluble in water, a ruthenium atom, and optionally a solvent molecule selected from an organic polar solvent and water, whereby the solvent molecule is bound to the ruthenium atom.
  • An active catalyst complex in the context of the present specification refers particularly to a compound comprising an optically active ligand that (again, the ligand) is insoluble in water, a ruthenium atom, at least one water molecule and a monohydride being bound to the ruthenium atom.
  • the solvent molecule can be substituted by the substrate molecule mentioned above in an aqueous solvent system, and one half of the substrate molecule's double bond is hydrogenated by the monohydride, while the other half of the double bond may be hydrogenated by elementary hydrogen solved in the solvent system, wherein the hydrogenation is performed.
  • optically active ligand in the context of the present specification refers to a compound that is capable of binding to the ruthenium atom described above and is characterized by an optical activity, wherein optical activity or optical rotation is the turning of the plane of linearly polarized light as the light travels through the ligand. Accordingly, there are at least two enantiomeric forms of the optically active ligand, wherein each form rotates the plane of light in an opposite direction.
  • insoluble in water in the context of the present specification particularly refers to a solubility of an entity of below 0.02 mol/l, 0.01 mol/l, 0.005 mol/l or 0.001 mol/I at 25°C.
  • a monohydride in the context of the present specification refers to a hydrogen atom with one electron, whereby this electron participates in the bonding between the hydrogen atom and the ruthenium atom, while the other electron of the bond is provided by the ruthenium atom.
  • a solubilizer in the context of the present specification refers to a compound or composition, the presence of which increases the solubility in water of poorly soluble or non-soluble compounds or compositions.
  • the solubilizer is a non-ionic surfactant or an organic solvent that is miscible with water.
  • the activation solvent system comprises at least 50 % (v/v), 75 % (v/v) 80 % (v/v), 90 % (v/v), 99 % (v/v) or 100 % (v/v) water.
  • the precatalyst complex comprises a monohydride bound to the ruthenium complex.
  • Such precatalyst complex with bound monohydride can be converted to an active catalyst complex by the method for converting a precatalyst complex to an active catalyst complex according to the invention, with the exception that the method may be performed without solving hydrogen in the activation solvent system.
  • the acid is characterized by a pKa value of ⁇ 0.
  • the acid is a hydrogen acid. In some embodiments, the acid is characterized by formula HX, wherein X is the corresponding anionic base.
  • the acid deprotonates after solving in the activation solvent system, whereby the resulting corresponding anionic base of the acid binds to the ruthenium atom.
  • the nature of the bond between the ruthenium atom and the corresponding anionic base is covalent or coordinative in nature.
  • the acid is selected from the group comprised of sulphuric acid, nitric acid, sulfonic acid, perchloric acid, perbromic acid, fluorosulfuric acid, hydrobromic acid, hydrochloric acid, hydriodic acid and fluoroboric acid.
  • an acid solution is solved in the activation solvent system, wherein the acid solution is characterized by an acid concentration of 0.05 N, 0.1 N, 0.2 N, 0.3 N, 0.4 N, 0.5 N, 0.6 N, 0.7 N, 0.8 N, 0.9 N, 1 N, 1.5 N, 2 N, 2.5 N or 3 N.
  • the optically active ligand is a bidentate ligand or a monodentate ligand.
  • one bidentate ligand is bound to the ruthenium atom.
  • two monodentate ligands are bound to the ruthenium atom.
  • the nature of the bond between the ruthenium atom and the monodentate ligand or the bidentate ligand is covalent or coordinative in nature.
  • the catalyst complex is characterized by two water molecules bound to the ruthenium atom.
  • the precatalyst complex is characterized by formula I wherein
  • the organic solvent molecule is selected from methanol, trichloromethane, dichloromethane, ethanol, trifluoroethanol, n-propanol, 2-propanol, n-butanol, 2-butanol, n-pentanol, 2-pentanol, 3-pentanol, n-hexanol, 2-hexanol 3-hexanol, hexane, heptane and octane.
  • the active catalyst complex is characterized by formula II wherein L 1 , L 2 have the same meaning as described above, and X is R 1 described above or the corresponding anionic base to the acid HX described above.
  • the water molecule bound to the ruthenium leaves the catalyst as oxonium (H 3 O + ), when being substituted against the substrate molecule.
  • the optically active ligand is selected from the group comprised of:
  • the solubilizer is a polar organic solvent or a surfactant that is capable of forming micelles in water and is resistant to hydrolysis at pH ⁇ 2.
  • the solubilizer is a non-ionic surfactant, particularly an alkylglycoside, more particularly D-Glycopyranoside C9-C11 alkyl (CAS No. 132778-08-6, obtained from Cognis/BASF AG).
  • a surfactant in the context of the present specification refers to an amphiphilic compound that lowers the surface tension of a liquid, particularly of water.
  • a micelle in the context of the present specification refers to a supramolecular spherical aggregate of surfactant molecules dispersed in a liquid, particularly in water. Such aggregate exhibits a hydrophilic surface that is in contact to the liquid and formed by hydrophilic heads of the surfactant molecules and a lipophilic or hydrophobic core that is shielded from the liquid and formed by the lipophilic tail group of the surfactant molecules.
  • the surfactant is a detergent or tenside comprising a hydrophilic head group and a lipophilic tail group.
  • the hydrophilic head group is an anionic group, wherein the anionic group does not comprise a double bound.
  • the hydrophilic head is a non-ionic group selected from the group comprised of fatty alcohols, polyoxyethylene glycol alkyl ethers, polyoxypropylene glycol alkyl ethers and glucosides.
  • the hydrophilic head is a cationic group select from tetraalkylammonium and quaternary ammonium cations.
  • the lipophilic tails group consists of hydrocarbons.
  • the lipophilic head is selected from a C 3 -C 30 -alkyl, -aryl, -heterocyclyl, -heteroaryl and -carbocyclyl.
  • alkyl or alkyl group in the context of the present specification signifies a saturated hydrocarbon moiety, which may be linear, branched, cyclic or cyclic with linear or branched side chains.
  • alkyl includes partially unsaturated hydrocarbons such as propenyl. Examples are n- or isobutyl, n- or cyclohexyl, heptyl, octyl, dodecyl and octadecyl.
  • alkyl may extend to alkyl groups linked or bridged by hetero atoms such as N, S or O.
  • aryl in the context of the present specification signifies a cyclic aromatic hydrocarbon.
  • Heteroaryl in the context of the present invention are aryls that comprise nitrogen, oxygen or sulfur atoms. Examples of heteroarly are pyrrol, 1,2- or 1,3-diazole, thiadiazole (e.g. 1,2,5-, 1,2,3- ), furane, thiophene, indole and its O- and S-homologues, indolizine or pyridine.
  • heterocyclyl in the context of the present specification signifies chains or rings, or combinations thereof, of carbon, oxygen, nitrogen and/or sulphur atoms that are connected by single or double bonds.
  • heterocyclyl moieties are a morpholino moiety and a piperidinyl moiety.
  • carbocyclyl in the context of the present specification signifies rings of carbon or a combination of chains and rings of carbon that are connected by single bonds.
  • Examples for carbocyclyls are cyclopropane, cyclobutane, cyclopentane, cyclohexane and cycloheptane.
  • the surfactant has a decomposition rate constant at pH 2 of not higher than 10 s -1 , 1 s -1 , 0.1 s -1 , 0.01 s -1 or 0.001 s -1 at 25 °C.
  • the surfactant is non-ionic.
  • a non-ionic surfactant in the context of the present specification refers particularly to a surfactant without dissociative groups, particularly without a carboxy group.
  • the surfactant is an alkylglycoside.
  • An alkylglycoside in the context of the present specification refers to a compound comprising a C 1 -C 20 alkyl alcohol moiety as lipophilic tail group and a sugar moiety as hydrophilic head group, wherein the anomeric hydroxyl group of the sugar and the hydroxyl group of the alcohol form an actetal bond.
  • the surfactant is the alkylglycoside D-Glycopyranoside C9-C11 alkyl (CAS No. 132778-08-6).
  • the lipophilic tail group is a C 8 -C 14 alkyl alcohol moiety.
  • the sugar moiety comprises a monosaccharide or an oligosaccharide.
  • the monosaccharide is selected from glucose, fructose, mannose, ribose, galactose and ribulose.
  • the oligosaccharide is selected from sucrose, maltose, cellobiose or raffinose.
  • the surfactant has a critical micellar concentration (CMC) value of ⁇ 10 mM, more preferably ⁇ 1 mM, most preferably ⁇ 0.25 mM, wherein CMC specifies the lowest concentration of the surfactant in water at which spherical micelles are formed at 25°C and 1 bar.
  • CMC critical micellar concentration
  • the surfactant is provided in the activation solvent system in a concentration equal or above the surfactant's critical micelle concentration.
  • a method for obtaining a catalyst composition comprising the steps of:
  • a catalyst composition in the context of the present specification refers particularly to a compound or composition that can lower the activation energy of a chemical reaction and accelerate the reaction by at least 3 orders of magnitude, particularly a hydrogenation reaction in presence of elementary hydrogen.
  • An optically inactive ligand in the context of the present specification refers to a compound that is capable of binding to the metal atom described above and that has no optical activity.
  • the optically inactive ligand is selected from the group comprised of 1,5-cyclooctadiene, acetyl acetonate, (1,5-cyclooctadien)bismethylallyl, bis(ethylcyclopentadienyl), bis(pentamethylcyclopentadienyl), p-cymene, diacetato, norbonadiene, cyclohexadiene, cylcoheptandiene, para-methadiene, ⁇ -Phellandiene and benzol.
  • optically active ligand optically active ligand, acid, solubilizer, surfactant and micelle have the same meaning as described above.
  • the solubilizer is a polar organic solvent miscible in water over a range of 1 part solvent: 99 parts water to 1 part solvent: 5 parts water.
  • the solubilizer is a preparation surfactant that is capable of forming micelles in water and resistant to hydrolysis at pH ⁇ 2.
  • the preparation solvent system comprises not more than 50 % (v/v), 25 % (v/v), 20 % (v/v), 10 % (v/v) or 1 % (v/v) polar organic solvent.
  • the preparation solvent system comprises at least 50 % (v/v), 75 % (v/v) 80 % (v/v), 90 % (v/v), 99 % (v/v) or 100 % (v/v) water.
  • the second catalyst composition further comprises a water molecule bound to the ruthenium atom.
  • the nature of the bond between the ruthenium atom and the water molecule is covalent or coordinative in nature.
  • the second catalyst composition comprises two water molecules bound to the ruthenium atom.
  • the second catalyst composition is further reacted with elementary hydrogen, yielding a catalyst composition with a monohydride bound to the ruthenium atom.
  • the nature of the bond between the ruthenium atom and the monohydride is covalent or coordinative in nature.
  • Such second catalyst composition is suitable to perform a catalytic cycle as described above.
  • the preparation surfactant is provided in the preparation solvent system in a concentration equal or above the surfactant's critical micelle concentration.
  • the second catalyst composition is insoluble in water.
  • the preparation solvent system further comprises a pH-control agent.
  • a pH-control agent in the context of the present specification refers to a compound by which the pH of an aqueous solution can be altered.
  • Such pH-control agent may be an acid, a base or ion exchange resin.
  • a pH control agent may also be a buffer system comprising a combination of acids and bases that are selected such that the pH value of a composition comprising the buffer changes less upon addition of an acid or a base than in a corresponding composition without the buffer system.
  • the preparation surfactant has a critical micellar concentration (CMC) value of ⁇ 10 mM, more preferably ⁇ 1 mM, most preferably ⁇ 0.25 mM, wherein CMC specifies the lowest concentration of the surfactant in water at which spherical micelles are formed at 25°C and 1 bar.
  • CMC critical micellar concentration
  • the preparation surfactant is non-ionic.
  • the preparation surfactant is an alkylglycoside.
  • alkylglycoside has the same meaning as described above.
  • the prepartion surfactant is D-Glycopyranoside C9-C11 alkyl (CAS No. 132778-08-6, obtained from Cognis/BASF AG).
  • the acid is characterized by a pKa value of ⁇ 0.
  • the acid is a hydrogen acid.
  • the acid is characterized by formula HX, wherein X is the corresponding anionic base.
  • the acid deprotonates after solving in the preparation solvent system, whereby the resulting corresponding anionic base of the acid binds to the ruthenium atom comprised within the second catalyst composition.
  • the nature of the bond between the ruthenium atom and the corresponding anionic base is covalent or coordinative in nature.
  • the acid is selected from the group comprised of sulphuric acid, nitric acid, sulfonic acid, perchloric acid, perbromic acid, fluorosulfuric acid, hydrobromic acid, hydrochloric acid, hydriodic acid, and fluoroboric acid.
  • an acid solution is solved in the preparation solvent system, wherein the acid solution is characterized by a concentration of 0.1 N, 0.2 N, 0.3 N, 0.4 N, 0.5 N, 0.6 N, 0.7 N, 0.8 N, 0.9 N, 1 N, 1.5 N, 2 N, 2.5 N or 3 N.
  • Hydrogenating a double bond in context of the present specification refers to a chemical reaction, wherein the double bond is converted to a single bond and hydrogen is added to both partners of the former double bond.
  • the substrate has a molecular mass of more (>) than 28, 34, 60 or 72 g/mol.
  • the substrate molecule is organic molecule comprising at least 5 atoms of a molecular mass of 12 or higher, and comprising a carbonyl (keto, aldehyde) or imine group.
  • catalytic composition solubilizer and optically active ligand have the same meaning as described above.
  • the hydrogenation is performed at pH ⁇ 2 by further solving an acid in the reaction solvent system.
  • acid has the same meaning as described above.
  • the reaction solvent system comprises at least 50 % (v/v), 75 % (v/v) 80 % (v/v), 90 % (v/v), 99 % (v/v) or 100 % (v/v) water.
  • the acid is a hydrogen acid.
  • the acid is characterized by a pKa value of ⁇ 0.
  • the acid is selected from the group comprised of sulphuric acid, nitric acid, sulfonic acid, perchloric acid, perbromic acid, fluorosulfuric acid, hydrobromic acid, hydrochloric acid, hydriodic acid and fluoroboric acid.
  • the solubilizer is a polar organic solvent or a reaction surfactant that is capable of forming a micelle in water and resistant to hydrolysis at pH ⁇ 2.
  • the term surfactant has the same meaning as described above.
  • the reaction solvent system comprises not more than 50 % (v/v), 25 % (v/v), 20 % (v/v), 10 % (v/v) or 1 % (v/v) polar organic solvent.
  • the reaction surfactant is provided in the reaction solvent system in a concentration equal or above the surfactant's critical micelle concentration.
  • the reaction surfactant has a critical micellar concentration (CMC) value of not larger than 10 mM, more preferably 1 mM, most preferably 0.25 mM, wherein CMC specifies the lowest concentration of the surfactant in water at which spherical micelles are formed at 25°C and 1 bar.
  • CMC critical micellar concentration
  • reaction surfactant is non-ionic.
  • the reaction surfactant is an alkylglycoside.
  • alkylglycoside has the same meaning as described above.
  • reaction surfactant is D-Glycopyranoside C9-C11 alkyl (CAS No. 132778-08-6, obtained from Cognis/BASF AG).
  • reaction surfactant is identical to the preparation surfactant described above.
  • the substrate molecule comprises at least 3 carbon atoms.
  • the substrate molecule is soluble in the aqueous phase of the second solvent system.
  • the substrate molecule is an aliphatic or cyclic, saturated or unsaturated compound having a carbonyl or imine group such ketones, aldehydes, aldimines, ketimines, cabon acid or esters.
  • reaction solvent system further comprises a pH-control agent.
  • pH-control agent has the same meaning as described above.
  • the hydrogenation is performed at temperatures between 20°C and 200°C, preferably between 80°C and 180°C, more preferably between 100°C and 140°C, most preferable between 110°C and 130°C.
  • reaction solvent system does not comprise organic solvents.
  • the hydrogenating is an asymmetric hydrogenating reaction.
  • Asymmetric hydrogenating in the context of the present specification shall mean that adding hydrogen to the double bond of a substrate molecule generates a new chiral centre, and that the asymmetric adding results in an addition product in enantiomeric excess (ee) of 50 %, 90 % or 95 %.
  • Enantiomeric excess is defined as the absolute difference between the mole fraction of each enantiomer. For example an enantiomeric excess of 90% means an addition product with 95 n/n% of one enantiomer and 5 n/n% of the opposite enantiomer.
  • the catalyst composition is obtained by a method according to the second aspect or comprises an active catalyst complex obtained by a method according to the first aspect of the invention.
  • the method for hydrogenating a double bond further comprises solving an acid in the reaction solvent system.
  • the acid is a hydrogen acid.
  • the acid is selected from the group comprised of sulphuric acid, nitric acid, sulfonic acid, perchloric acid, perbromic acid, fluorosulfuric acid, hydrobromic acid, hydrochloric acid, hydriodic acid and fluoroboric acid.
  • an acid solution is solved in the reaction solvent system, wherein the acid solution is characterized by a concentration of 0.1 N, 0.2 N, 0.3 N, 0.4 N, 0.5 N, 0.6 N, 0.7 N, 0.8 N, 0.9 N, 1 N, 1.5 N, 2 N, 2.5 N or 3 N.
  • the substrate molecule is selected from the group comprised of:
  • the product of the hydrogenating is selected from the group comprised of:
  • a reaction mixture comprising
  • solubilizer surfactant, reaction surfactant, catalyst complex, catalyst composition and substrate molecule have the same meaning as described above.
  • the solvent system comprises at least 50 %, at least 75 % or at least 95 % water or at least 100 % water.
  • the solubilizer is a polar organic solvent or a reaction surfactant as specified in the above embodiments.
  • the solvent system comprises not more than 50 % (v/v), 25 % (v/v), 20 % (v/v), 10 % (v/v) or 1 % (v/v) polar organic solvent. In some embodiments, the reaction mixture does not comprise organic solvents.
  • the substrate molecule is any of
  • every embodiment that defines an optically active ligand may be combined with every embodiment that defines S, R 1 , R 2 or X to characterize a group of precatalyst or active catalyst complexes or compositions of the invention or a single complex or composition of the invention with different properties.
  • the invention is further characterized, without limitations, by the following examples, from which further features, advantages or embodiments can be derived.
  • the examples do not limit but illustrate the invention.
  • the catalyst solution obtained according to Preparation III, but with (S)-SYNPHOS as chiral ligand was placed into an autoclave in the presence of 50 ml of degassed water, 275 ⁇ l of a 45 wt. % hydrobromic acid solution, 1g alkylpolyglucoside as well as 5.4*10 -3 mol of hydroxyacetone under a hydrogen atmosphere of 4.2 bar pressure.
  • the reaction mixture was stirred and heated at 125 °C for 6 hours.
  • the solution was extracted with ethyl acetate.
  • the extract was dried on anhydrous magnesium sulfate.
  • the enantiomeric excess was then determined by chiral GC (FS LIPODEX A). As a result, the yield was 100% and the purity of the (S)-form of 1,2-propanediol was more than 97 % ee.
  • the catalyst solution obtained according to Preparation II, but with (S)-SEGPHOS as chiral ligand was placed into an autoclave in the presence of 50 ml of degassed water, 275 ⁇ l of a 45 wt. % hydrobromic acid solution, 1g alkylpolyglucoside as well as 5.4*10 -3 mol of hydroxyacetone under a hydrogen atmosphere of 4.2 bar pressure.
  • the reaction mixture was stirred and heated at 125 °C for 3 hours.
  • the solution was extracted with ethyl acetate.
  • the extract was dried on anhydrous magnesium sulfate.
  • the enantiomeric excess was then determined by chiral GC as in Example 1.
  • the conversion was 55 % and the purity of the (S)-form of 1,2-propanediol was more than 97 % ee, by a yield of 100 % (i.e. 100 % of the 55 % of the starting materials which were converted belong to the desired product species, which means that no side reactions occurred; the product showed an enantiomeric excess of 97 % ee).
  • the catalyst solution obtained according to Preparation II, but with (R)-SYNPHOS as chiral ligand is placed into an autoclave in the presence of, 30ml of heptane, 20 ml of degassed water, 110 ⁇ l of a 45 wt. % hydrobromic acid solution, 1g alkylpolyglucoside as well as 5.4*10 -3 mol of hydroxyacetone under a hydrogen atmosphere of 4.7 bar pressure.
  • the reaction mixture was stirred and heated at 125 °C for 3 hours.
  • the solution was extracted with ethyl acetate.
  • the extract was dried on anhydrous magnesium sulfate.
  • the enantiomeric excess was then determined by chiral GC as in Example 1.
  • the yield was 90 % and the purity of the (R)-form of 1,2-propanediol was more than 97 % ee.
  • the catalyst solution obtained according to Preparation II, but with (S)-SYNPHOS as chiral ligand is placed into an autoclave in the presence of, 25ml of ethanol, 30 ml of degassed water, 165 ⁇ l of a 45 wt. % hydrobromic acid solution, 2ml alkylpolyglucoside as well as 0,51 g of hydroxyacetone under a hydrogen atmosphere of 1.1 bar pressure.
  • the reaction mixture was stirred and heated at 60 °C for 6 hours.
  • the solution was extracted with ethyl acetate.
  • the extract was dried on anhydrous magnesium sulfate.
  • the enantiomeric excess was then determined by chiral GC as in Example 1. As a result, the yield was 100% and the purity of the (S)-form of 1,2-propanediol was more than 97 % ee.
  • the catalyst solution obtained according to Preparation , but with (S)-SYNPHOS as chiral ligand was placed into an autoclave in the presence of, 25ml of ethanol, 30 ml of degassed water, 165 ⁇ l of a 45 wt. % hydrobromic acid solution, 2ml alkylpolyglucoside as well as 0,51 g of hydroxyacetone under a hydrogen atmosphere of 1.1 bar pressure.
  • the reaction mixture was stirred and heated at 60 °C for 3 hours.
  • the solution was extracted with ethyl acetate.
  • the extract was dried on anhydrous magnesium sulfate.
  • the enantiomeric excess was then determined by chiral GC as in Example 1.
  • the yield was 100 % and the purity of the (S)-form of 1,2-propanediol was more than 97 % ee.
  • the catalyst solution obtained according to Preparation III, but with (S)-SYNPHOS as chiral ligand was placed into an autoclave in the presence of, 25 ml of ethanol, 30 ml of degassed water, 165 ⁇ l of a 45 wt. % hydrobromic acid solution, 2ml alkylpolyglucoside as well as 0,51 g of hydroxyacetone under a hydrogen atmosphere of 1.1 bar pressure.
  • the reaction mixture was stirred and heated at 60 °C for 3 hours.
  • the solution was extracted with ethyl acetate.
  • the extract was dried on anhydrous magnesium sulfate.
  • the enantiomeric excess was then determined by chiral GC as in Example 1.
  • the conversion was 100 % and the purity of the (S)-form of 1,2-propanediol was more than 97 % ee.
  • the catalyst solution obtained according to Preparation, but with (S)-SYNPHOS as chiral ligand was placed into an autoclave in the presence of, 25 ml of ethanol, 30 ml of degassed water, 165 ⁇ l of a 45 wt. % hydrobromic acid solution, 2 ml alkylpolyglucoside as well as 0,51 g of hydroxyacetone under a hydrogen atmosphere of 1.1 bar pressure.
  • the reaction mixture was stirred and heated at 60 °C for 3 hours.
  • the solution was extracted with ethyl acetate.
  • the extract was dried on anhydrous magnesium sulfate.
  • the enantiomeric excess was then determined by chiral GC as in Example 1. As a result, the conversion was 91% and the purity of the (S)-form of 1,2-propanediol was more than 97 % ee.
  • the catalyst solution obtained according to Preparation II, but with (S)-SYNPHOS as chiral ligand is placed into an autoclave in the presence of, 25 ml of ethanol, 37,5 ml of degassed water, 165 ⁇ l of a 45 wt. % hydrobromic acid solution, 2 ml alkylpolyglucoside as well as 0,428 g of hydroxyacetone under a hydrogen atmosphere of 1.1 bar pressure.
  • the reaction mixture was stirred and heated at 80 °C for 6 hours.
  • the solution was extracted with ethyl acetate.
  • the extract was dried on anhydrous magnesium sulfate.
  • the enantiomeric excess was then determined by chiral GC as in Example 1. As a result, the conversion was 90 % and the purity of the (S)-form of 1,2-propanediol was more than 97 % ee.
  • the catalyst solution obtained according to Preparation III, but with (S)-SYNPHOS as chiral ligand is placed into an autoclave in the presence of, 25 ml of ethanol, 37,5 ml of degassed water, 165 ⁇ l of a 45 wt. % hydrobromic acid solution, 2 ml alkylpolyglucoside as well as 0,428 g of hydroxyacetone under a hydrogen atmosphere of 1.1 bar pressure.
  • the reaction mixture was stirred and heated at 80 °C for 6 hours.
  • the solution was extracted with ethyl acetate.
  • the extract was dried on anhydrous magnesium sulfate.
  • the enantiomeric excess was then determined by chiral GC as in Example 1. As a result, the conversion was 90% and the purity of the (S)-form of 1,2-propanediol was more than 97 % ee.

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EP13157998.9A 2013-03-06 2013-03-06 Wasserunlösliche Rutheniumkatalysatorzusammensetzung zur Verwendung bei wässrigen Hydrierungsreaktionen Withdrawn EP2774674A1 (de)

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EP13157998.9A EP2774674A1 (de) 2013-03-06 2013-03-06 Wasserunlösliche Rutheniumkatalysatorzusammensetzung zur Verwendung bei wässrigen Hydrierungsreaktionen
HUE14713774A HUE059503T2 (hu) 2013-03-06 2014-03-05 Vizes hidrogénezési reakciók vízoldhatatlan ruténium katalizátor kompozíció alkalmazásával
US14/772,393 US9433937B2 (en) 2013-03-06 2014-03-05 Water-insoluble ruthenium catalyst composition for use in aqueous hydrogenation reactions
EP14713774.9A EP2964384B1 (de) 2013-03-06 2014-03-05 Wässrigen hydrierungsreaktionen mit wasserunlöslicher ruthenium-katalysatorzusammensetzung
PCT/EP2014/054291 WO2014135605A1 (en) 2013-03-06 2014-03-05 Water-insoluble ruthenium catalyst composition for use in aqueous hydrogenation reactions
JP2015560679A JP6423805B2 (ja) 2013-03-06 2014-03-05 水系溶媒中の水素化反応に使用するための水不溶性ルテニウム触媒組成物
CN201480024756.8A CN105392563B (zh) 2013-03-06 2014-03-05 含水氢化反应中所使用的不溶于水的钌催化剂组合物
DK14713774.9T DK2964384T3 (da) 2013-03-06 2014-03-05 Vandige hydrogeneringsreaktioner ved anvendelse af en vanduopløselig Ruthenium-katalysatorsammensætning
ES14713774T ES2922331T3 (es) 2013-03-06 2014-03-05 Reacciones de hidrogenación acuosas que usan una composición de catalizar de rutenio insoluble en agua
PL14713774.9T PL2964384T3 (pl) 2013-03-06 2014-03-05 Wodne reakcje uwodorniania z zastosowaniem nierozpuszczalnej w wodzie kompozycji katalizatora rutenu
IL241130A IL241130B (en) 2013-03-06 2015-09-03 Composition of a water-insoluble ruthenium catalyst for use in aqueous hydrogenation reactions
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CN105622346A (zh) * 2014-11-04 2016-06-01 中国石油化工股份有限公司 一种由β-二酮固定床加氢制备β-二醇的方法
CN105622345A (zh) * 2014-11-04 2016-06-01 中国石油化工股份有限公司 一种制备β-二醇的方法

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CN105566068B (zh) * 2014-11-04 2018-05-11 中国石油化工股份有限公司 一种用于β-二酮加氢制备β-二醇的方法
US11356520B2 (en) * 2015-05-29 2022-06-07 Sound United, Llc. System and method for selecting and providing zone-specific media
KR20240074023A (ko) 2015-08-24 2024-05-27 아비오메드, 인크. 의료 장치 도입기용 지혈 밸브

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CN105622346A (zh) * 2014-11-04 2016-06-01 中国石油化工股份有限公司 一种由β-二酮固定床加氢制备β-二醇的方法
CN105622345A (zh) * 2014-11-04 2016-06-01 中国石油化工股份有限公司 一种制备β-二醇的方法

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US9758457B2 (en) 2017-09-12
PL2964384T3 (pl) 2022-10-24
US20160355454A1 (en) 2016-12-08
WO2014135605A1 (en) 2014-09-12
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EP2964384B1 (de) 2022-05-04
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